Title of article :
Monolith loop catalytic membrane reactor for Fischer–Tropsch synthesis Original Research Article
Author/Authors :
Michael C.J. Bradford، نويسنده , , Mure Te، نويسنده , , Allen Pollack، نويسنده ,
Issue Information :
روزنامه با شماره پیاپی سال 2005
Abstract :
A monolith loop catalytic membrane reactor (ML-CMR) concept for Fischer–Tropsch synthesis (FTS) was investigated by evaluating the performance of a P/Pt–Co/γ-Al2O3 catalyst in a prototype, tubular CMR and in a tubular, fixed-bed reactor (FBR). Although experimental data demonstrate that the selectivity to paraffins and the product yield per unit catalyst mass exhibited by the P/Pt–Co/γ-Al2O3 catalyst in the tubular CMR exceed those observed by the same catalyst in a tubular FBR, simple model calculations indicate that the ML-CMR product yield per unit reactor volume, at its present stage of development, is less than that for state-of-the-art multi-tubular fixed-bed and slurry-bubble column reactors.
Keywords :
Monolith loop , Fischer–Tropsch , Membrane reactor , Natural gas conversion
Journal title :
Applied Catalysis A:General
Journal title :
Applied Catalysis A:General